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    • 专利摘要:
    separation medium and methods especially useful for separating hydrocarbon emulsions in water having low interfacial stresses. separation means, separation modules and methods are provided for separating water from a hydrocarbon emulsion in water and include a fibrous non-woven coalescence layer to receive the eagle and hydrocarbon emulsion in water and include a coalescence layer fibrous nonwoven to receive the water and hydrocarbon emulsion and coalesces the water present in it as a discontinuous phase to reach the coalesced water droplets having a size of 1 mm or larger, and a fibrous, non-woven downstream retention layer of the coalescence layer having a high surface bet area of at least 90 m2 / g or sufficiently larger to maintain the size of the drops of coalesced water to allow its separation from the hydrocarbon.
    公开号:BR112012007819B1
    申请号:R112012007819-4
    申请日:2010-10-07
    公开日:2020-12-15
    发明作者:Farina Pangestu；Christine Stanfel
    申请人:Ahlstrom-Munksjö Oyj；
    IPC主号:
    专利说明:

    FIELD OF THE INVENTION
    [001] The modalities disclosed here relate, in general, to the means of separation and methods for separating hydrocarbon and water emulsions. In particularly preferred forms, the embodiments disclosed herein refer to the separation of water from a water-containing hydrocarbon fuel emulsion (e.g., diesel oil). BACKGROUND OF THE INVENTION
    [002] The need to separate water and hydrocarbon emulsions is ubiquitous; historically affects a wide variety of industries. The separation of hydrocarbon and water emulsions has conventionally involved systems that depend on single or multiple elements, new flow patterns, dissipation chambers, parallel metal plates, oriented wires, gas intrusion mechanisms and electrostatic charge. The balance of separation systems employs an element that contains a porous and fibrous coalescent medium through which the emulsion is passed and separated. Regardless of the system design, all water and hydrocarbon separation systems aim to collect emulsified drops in close proximity to facilitate coalescence. Coalescence and subsequent separation due to differences in densities between water and hydrocarbons are the mechanism behind all separation systems.
    [003] Conventionally known porous and fibrous coalescing media induce the separation of the emulsion in applications through the flow through the same general mechanism, regardless of the nature of the emulsion. The coalescence medium presents for the discontinuous phase of the emulsion of an energetically dissimilar surface from the continuous phase. As such, the surface of the medium serves to compete with the continuous phase of the emulsion for the discontinuous, or drops, phase of the emulsion. As the emulsion comes in contact with and progresses through the coalescing means, droplet partitions occur between the solid surface and the continuous phase. Drops adsorbed on the surface of the solid medium travel along fiber surfaces, and in some cases, wet the fiber surface. The more the emulsion flows through the medium, the discontinuous adsorbed phase encounters other drops associated with the media and the two coalesces. The coalescence - drop migration process continues once the emulsion moves through the medium.
    [004] A coalescence medium is therefore typically considered to be functionally successful in breaking a supplied emulsion if the discontinuous phase preferably adsorbs or repels and if the drop phase has been coalesced into drops at the exit point from means that are large enough to allow their separation from the continuous phase. Typically, the droplets separate from the continuous phase as a function of the density differences between the liquids involved. On the other hand, a coalescing medium is considered to be functionally unsuccessful to break an emulsion if the droplets remain small enough at the exit point from the means that they remain entrained by the continuous phase and fail to separate.
    [005] Conventional fibrous and porous coalescence media are known, which effectively remove more than 90% by weight of emulsified water from a hydrocarbon, when the hydrocarbon has an interfacial tension (y) above 0.025 N / m ( 25 dynes / cm) with water. If the hydrocarbon exhibits water-hydrocarbon interfacial tension less than 0.025 N / m (25 dynes / cm) (colloquially known as "hydrocarbons with sub-25 interfacial tension (0.025N / m)"), the water-hydrocarbon emulsion is considerably more tenacious and the ability of the prior art emulsion separation means to remove emulsified water dramatically decreases to the point where 40-100% by weight of emulsified water is allowed to pass to end use without removal.
    [006] A decrease in the interfacial tension of the hydrocarbon occurs when the hydrocarbon is dosed with tesnsoativos. In this regard, the main cause of the failure of the fibrous and porous coalescence medium of the technical state in hydrocarbon media with sub-25 interfacial tension (0.025N / m) is the presence of increased tensile activity. In cases of hydrocarbons with sub-25 interfacial tension (0.025N / m), separation of the emulsion requires more complex systems that often involve pleated grouped elements, flow path controllers, wraps, and dissipation chambers. The state of the art is replete with examples of complex systems designed to manage difficulty in separating hydrocarbon and water emulsions. Therefore, the need for a universal medium capable of separating emulsion regardless of the hydrocarbon and water interfacial tension or surfactant content is clear in the face of such complexity.
    [007] The role of deactivating the surfactant of the porous and fibrous medium of conventional coalescence includes drop size, drop stability, and surfaces. Surfactants are molecules that contain both hydrophilic and hydrophobic moieties. When present in a mixture of hydrocarbon and water, surfactants align at interfaces with the main hydrophilic group associated with the aqueous phase, and the final hydrophobic part extended to the oil phase. This is the lowest energy conformation of the surfactant, which results in the declining interfacial tension of hydrocarbon in water. As a result of the declining interfacial tension, an increased supply of energy input to the mixture of hydrocarbons and water will result in a greater surface area of interface, in the presence of a surfactant. Surface interface area is inversely proportional to the drop size in the discontinuous phase. Thus, in the presence of a surfactant, an increase in energy input will result in a smaller drop size distribution of the discontinuous phase than in the absence of a surfactant. In this sense, all means of separating fuel and water depend on physical interaction between drops of water and the means to effect the separation. Surfactants create small enough drops of water and many of them pass through the middle, without meeting this one. Surfactants also stabilize the separation emulsion so that the drops that impact the media are less susceptible to partition out of the fuel in the medium. Likewise, drops that impact other drops resist coalescing into the larger drops needed for successful separation. Finally, surfactants are associated with the surfaces of the medium and drops of water, and interfere with the unique surface interactions between the medium and the water that destabilize the water inside the fuel and allow its separation. Collectively, the result of mixing surfactants in a hydrocarbon is the deactivation of the porous and fibrous coalescence medium of the state of the art, and water escape for final use.
    [008] The need for a porous and fibrous coalescence medium that removes water regardless of the hydrocarbon interfacial tension has become substantially more accentuated with mandatory changes in diesel fuel quality. In 2007, through the Heavy Duty Highway Diesel Rule, the EPA determined respective particle (PM 2.5) and nitrogen oxide (NOx) reductions of 90% and 92%, with NOx subsidies to reduce to an additional 3 % in 2010. Upon release of the determination, post-treatment sulfur-sensitive exhaust was considered necessary to meet the 2007 emission targets. As a result, the 2007 Highway Rule also requires a drop in sulfur levels in diesel fuel to 97% at 15 ppm. The resulting ultra low sulfur diesel fuel (ULSD) has been stripped of its native lubrication and requires the addition of a surfactant to meet engine wear control requirements. ULSD consistently manifests hydrocarbons of sub-25 interfacial tension (0.025N / m) with water. EPA has determined diesel fuel requirements such as cascading effect on off-road, rail diesel, and marine fuels as part of EPA's stepped approach to emission control, indicating all non-gasoline and power generation fuels will converge to the over time in the sub-25 interfacial tension (0.025 N / m) (25 dynes / cm).
    [009] In addition, several government regulatory agencies in the United States have begun offering incentives for or simply determining minimum components in the biodiesel blend for commercial transport fuels. Biodiesel is a mixture of methyl esters of fatty acids derived from the catalytic caustic esterification of methanol from triglycerides derived from plants and animals. Biodiesel is a surfactant, and fuel mixtures containing as little as 2% biodiesel have interfacial stresses well below 25 dynes / cm (0.025N / m). As a result, the pool of fuel available for transporting non-gasoline and power generation is quickly transitioning to a region of interfacial tension where the state-of-the-art fuel emulsion separation medium fails to remove water from the hydrocarbon.
    [0010] Despite changes in the interfacial tension of fuel, water remains a fuel contaminant of concern regarding corrosion of steel engine components and promoting microbiological growth. All engines that do not use gasoline have the ability to separate fuel and water from the fuel system. In addition, engine emission compliance with the EPA 2007 Highway Rule depends primarily on high pressure fuel injection equipment that is extremely sensitive to water. This makes fuel dehydration of greater importance for systems designed to meet the 2007 EPA emission determinations that have generated a systemic change in fuel quality. Fuel consumption and operator interface requirements for engines dictate the need for small, light and easy to operate water separation systems. These needs often preclude the complex separation systems that are conventionally known. As a result, mandatory changes in fuel quality created a well-defined need for a fibrous and porous coalescent medium that removes water regardless of the hydrocarbon interfacial tension.
    [0011] Examples of new coalescence media are described in common property, co-pending U.S. Patent Application no. 12 / 014,864 filed on January 16, 2008 and entitled "Coalescence Media for Separation of Water- Hydrocarbon Emulsions" (the entire content of which is expressly incorporated by reference here and will be referred to below as "the US '864 order"). These media reach high surface area with necessary pore structure and permeability and effectively separate tenacious emulsions from water and surfactant containing hydrocarbons, such as biodiesel-ULSD mixtures without using complex separation systems. The state of the art medium often requires several layers to affect the unique function of separating hydrocarbon emulsions in water, with no guarantee of successful separation in high surfactant content, low hydrocarbon interfacial tension. In contrast, the medium described in US Patent Application no. 12 / 014,864 is formed as a single dry layer from a wet deposition process using homogeneously distributed wet deposit furniture, including cellulose or cellulosic fibers, synthetic fibers, fibrillated fibers with a high surface area and glass microfiber, and a synthetic material to reinforce the surface area, which successfully performs the unique function of separating water with a single layer of filtration media at low interfacial hydrocarbon tension.
    [0012] It is typical for any fibrous and porous coalescence medium to be part of a multilayer medium structure, in which some of the layers perform functions, except for separating the emulsion. In such cases, the layers may or may not be laminated together. Reasons for employing multiple layers may be due to concerns about the integrity of the medium and / or filtration needs. Regarding the integrity of the medium, multiple layers are used to support the fibrous and porous coalescence medium or the composite structure to protect the fibrous and porous coalescence medium from rotary speed pleating machines, and to protect end use from possible migration of fibers from other layers of the medium. Regarding filtration needs, multiple layers are used to add filtration capabilities, such as particle removal, dirt support or impurity adsorption for coalescing performance. Impurities can consist of asphaltenes, organic portions, salts, ions, or metals. In order to achieve the filtration objectives, as well as to protect the integrity of the medium, a layer on the side downstream of the coalescence medium in a multifunctional filtration medium is required.
    [0013] Incorporation of a coalescence medium in a structure of multi-functional and multilayer coalescence medium, with a layer on the side downstream of the coalescence layer creates the possibility of failure in the medium with high surfactant hydrocarbons (ie, subfacial tension) -25 (0.025N / m)) due to the re-emulsification of the previously coalesced drops. In this regard, the coalesced water droplets must be large enough to establish the flow of hydrocarbons, due to differences in densities, otherwise they will be loaded out of the separation device with the dry hydrocarbon and re-emulsified therein. The coalescence medium must, therefore, work to enlarge microgroots of water found in hydrocarbon emulsions and water with a high surfactant content in millimeter-sized coalesced water droplets, which can gravimetrically establish the dry hydrocarbon flow.
    [0014] For these reasons mentioned above, in hydrocarbons with high surfactant content, the performance of any coalescence layer in a multilayer medium can be drastically reduced by a medium that is conventionally used on the side downstream of the coalescence layer. Specifically, conventional media located on the side downstream of a coalescence layer includes wet cellulose deposition medium saturated with phenolic resin, blow-molded polyester, spun bonded, and blow-fused and spun bonded composites, and nylon bonded by wiring. Such conventional media can and drastically reduce the coalescence function of coalescence media in hydrocarbons containing high surfactant content. As an example, the reduction in performance that can be manifested through the use of such conventional means downstream of a coalescence layer can be between about 50 to 100% of emulsified water remaining in the hydrocarbon and, thus, being passed to the final use of hydrocarbon due to the reduction in the size of the drops of the previously coalesced water drops.
    [0015] Therefore, it would be desirable if new media options to serve as layers placed on the side downstream of a coalescence medium could be provided so that it performs required support and protection functions, as well as exhibiting sufficiently larger surface area to adsorption of water to minimize re-emulsification. In this regard, it would be especially desirable if a medium serving as a downstream layer of a coalescence layer that not only performs its traditional support and protective papers, but also provides a larger surface area for water adsorption than the layer of coalescence. Such a downstream layer would serve to expand the flow path available to the water, and, consequently, induce the Venturi effect and reduce the speed of the water in relation to the hydrocarbon. Such a speed reduction, in turn, would increase the water pressure inside the layer downstream, thus forcing the hydrocarbon out of the layer. These factors would serve to further separate water from hydrocarbon and, thus, further facilitate water coalescence. This is highly desirable for separation applications involving surfactant-containing hydrocarbons. Therefore, it is additionally desirable to develop means capable of providing support and protection functions required from the means placed on the side downstream of a coalescence layer in a multilayer coalescence medium that provide greater surface area for water adsorption than those available. within the coalescence layer.
    [0016] It is towards fulfilling such desirable attributes that the present invention is directed. SUMMARY OF EXEMPLARY MODALITIES
    [0017] According to one aspect, the embodiments disclosed herein provide separation means for separating water from a water and hydrocarbon emulsion comprising a fibrous non-woven coalescence layer to receive the hydrocarbon and water emulsion and coalescing the present water in this as a discontinuous phase to reach coalesced water droplets having a size of 1 mm or larger, and a fibrous non-woven droplet retention layer downstream of the coalescence layer having a high BET surface area of at least 90 m2 / g or large enough to maintain the size of the coalesced water droplets to allow the separation of this from the hydrocarbon.
    [0018] In certain preferred forms, the drop retention layer of the separation medium will have a high BET surface area of at least 95 m2 / g, more preferably, of at least 100 m2 / g, or greater.
    [0019] The droplet retention layer can comprise a mixture of fibers having a high BET surface area and fibers having a low BET surface area and / or can comprise a resin binder. If a resin binder is provided, it preferably includes a polar chemical group.
    [0020] In accordance with certain embodiments, the separation means may comprise at least one additional layer positioned between the coalescence layers and the droplet retaining layers. For example, at least one additional layer can be positioned upstream and / or downstream of the droplet retaining layer to provide the separation means with desired physical properties.
    [0021] Modules for separating water from a water and hydrocarbon emulsion may be provided having a housing provided with an emulsion inlet and respective outlets for water and dehydrated hydrocarbons, the housing being provided with a means of separating these. The separation means provided in the housing preferably comprise a layer of fibrous non-woven coalescence to receive the water and hydrocarbon emulsion and to coalesce the water present therein as a discontinuous phase to reach the coalesced water droplets having a size of 1 mm or greater, and a fibrous, non-woven droplet retention layer downstream of the coalescence layer having a high BET surface area of at least 90 m2 / g or sufficiently larger to maintain the size of the coalesced water droplets to allow separation of this from the hydrocarbon.
    [0022] In accordance with yet another aspect, the modalities disclosed herein provide methods for separating water from a water and hydrocarbon emulsion by passing a water and hydrocarbon emulsion through a non-woven fibrous coalescence layer, in order to coalescing the water present in this as a discontinuous phase to reach the coalesced water droplets having a size of 1 mm or larger and then passing the hydrocarbon and the coalesced water droplets, although a droplet retention layer downstream having a high BET surface area of at least 90 m2 / g or sufficiently larger to maintain the size of the coalesced water droplets. The droplets of coalesced water can then be separated from the hydrocarbon (for example, by differences in densities between them). Preferably, at least 90% by weight of the water in the emulsion is coalesced into drops of water with a size of 1 mm, or larger by the coalescence layer.
    [0023] In preferred embodiments, the hydrocarbon has an interfacial tension (y) of less than 0.025 N / m (25 dynes / cm) (i.e., a sub-25 hydrocarbon (0.025N / m)). The hydrocarbon can thus be a liquid fuel (for example, a biodiesel fuel), which comprises a surfactant. BRIEF DESCRIPTION OF THE ANNEXED DRAWINGS
    [0024] These and other features and advantages will be better and more fully understood by reference to the following detailed description of exemplary non-limiting exemplary modalities in conjunction with the drawings of which:
    [0025] FIGURE 1 is a schematic cross-sectional view of a water and hydrocarbon separation system that incorporates the separation means of the present invention; and
    [0026] FIGURE 2 is a schematic enlarged cross-sectional view of an exemplary embodiment of the separation means according to the present invention as taken along line 2-2 in Figure 1. DEFINITIONS
    [0027] As used here and in the appended claims, the terms below are intended to have the definitions as follows.
    [0028] An "emulsion of hydrocarbons in water" is an emulsified mixture of immiscible water and liquid hydrocarbons.
    [0029] "Fiber" means a fibrous or filamentary filament of extreme or indefinite length.
    [0030] "Staple fibers" means a fiber, which has been cut to define relatively short segments of individual predetermined lengths.
    [0031] "Fibrous (a)" means a material that is composed predominantly of fibers and / or staple fibers.
    [0032] "Nonwoven (a)" means a set of fibers and / or staple fibers in a weft or felt that are randomly interlocked mechanically and / or tangled together.
    [0033] "Synthetic fiber" and / or "artificial fiber" refers to chemically produced fiber made from fiber-forming substances, including polymers synthesized from chemical compounds and modified or transformed into a natural polymer. Such fibers can be produced by conventional production techniques such as casting-spinning, solution-spinning and, similar to filament.
    [0034] The "natural fiber" is a fiber obtained from animal, mineral or vegetable origins.
    [0035] "BET surface area" means the surface area (m2) per unit weight (g) of a solid material calculated, generally, according to the Brunauer-Emmett-Teller (BET) methodology as described more fully in S Brunauer et al., J. Am. Chem. Soc., 1938, 60, 309 (the entire content of which is expressly incorporated by reference here), except for the fact that water vapor at 21 ° C was employed. (See also the description of Test Methods in the Examples below).
    [0036] "High BET" means a material having a BET surface area of 90 m2 / g or greater, more preferably a BET surface area of 95 m2 / g or greater, and more preferably, a BET surface area of 100 m2 / g or greater.
    [0037] "Low BET" means a material having a BET surface area of less than 90 m2 / g.
    [0038] A "sub-25 hydrocarbon (0.025N / m)" is a liquid hydrocarbon with an interfacial tension (y) of less than 0.025 N / m (25 dynes / cm). DETAILED DESCRIPTION
    [0039] The attached FIGURE 1 schematically represents an exemplary module 10 incorporating the present invention. In this regard, module 10 is provided with a housing 12 having an inlet 12-1 through which a flow of liquid from a fuel-in-water emulsion can be introduced. Housing 12 also includes outlets 12-2 and 12-3 to allow the dehydrated (dry) fuel and water flows, respectively, to be discharged from the separation following the housing.
    [0040] The housing 12 includes an interior space 12-4 to support a separation means 14. In one embodiment shown, the separation means 14 is in the form of a generally cylindrical structure comprised of a number of longitudinally oriented pleats. Other structural forms of the separation means 14 are, of course, possible, for example, spiral-wound sheets. The fuel-in-water emulsion thus enters the core 14-1 of the medium 14 and then passes through it. As is well known, due to differences in densities, coalesced water collects at the bottom of the housing, and is discharged via outlet 12-3. Dehydrated (dry) fuel is, in turn, discharged via outlet 12-2.
    [0041] As is perhaps best shown in the attached FIGURE 2, the separation means 14 is a multilayer structure comprised of at least one layer of non-woven fibrous coalescence 16 positioned upstream of a layer of non-woven fibrous droplet retention 18. The coalescence layer 16 and the drop retention layer can be positioned immediately adjacent to each other, and can, if desired, be physically laminated or physically connected to each other (for example, by any suitable technique known in the art, such as needle piercing, adhesives, air jet entanglement and the like). Alternatively, one or more intermediate layers 20 can optionally be interposed between the upstream coalescence layer 16 and the downstream drop retention layer 18. The various layers 16, 18 and, optionally, 20 can also be physically adjacent to each other or they can be laminated or otherwise connected to each other by any suitable technique known in the art.
    [0042] In addition (or alternatively) one or more face layers 22 may be provided upstream of the coalescence layer 16, while one or more support layers 24 may be provided downstream of the droplet retention layer 18. The layers 20, 22 and 24 are selected for various functional attributes, and need not necessarily be non-woven structures. Of course, such additional layers 20, 22 and / or 24 should not adversely affect the drop retention functionality of the drop retention layer 18.
    [0043] The layer of the coalescence medium can be a single layer or a multilayer structure. A preferred embodiment is a three-layer structure having an upstream layer, a coalescence layer in an intermediate position, and a downstream drop retention layer. The droplet retention layer can be laminated with the layer of the coalescence medium on a single sheet of the separation medium. The upstream layer can be a filter layer or a second layer of the coalescing medium. The upstream layer of the medium is preferably provided for particulate filtration and / or to support the structure and / or to physically protect the droplet retention layer 18. Tests indicated that the upstream non-woven nature had some influence on the coalescence performance of the composite. The results presented here include samples involving five separate support layers upstream. Upstream layers were selected for maximized coalescent droplet size and specific filtration needs, such as dirt-carrying capacity, asphaltene adsorption, and particle removal efficiency.
    [0044] The coalescence layer 16 of the separation medium 14 can be of any suitable type. In this regard, the coalescence layer is selected to coalesce a discontinuous aqueous phase of the fuel-in-water emulsion in the order of 0.01 - 500 micrometers in discrete drops of water having sizes of at least about 1 millimeter to about 10 millimeters . This coalescence of the discontinuous aqueous phase in discrete drops of water occurs when the emulsion passes through the coalescence layer 16.
    [0045] Coalescence layer 16 has a high surface area for water adsorption, creating a greater path length for water than the other components of the emulsion. This difference in path length translates into the different elution times for water and the other components of the emulsion, which results in phase enrichment and water coalescence. The separation of water out of the emulsion occurs when gravimetrically coalesced water droplets establish the flow while leaving the side downstream of the medium. Decanting occurs because water is more dense than hydrocarbons. In order to establish effectively in a flow system, coalesced water droplets must often overcome the flow of the purified hydrocarbon, which in many cases is contrary to the movement of the droplets. As such, the size of the water droplets is critical to the success of coalescing media. Successful separation is favored by larger drops of water. A particularly preferred medium that can be employed satisfactorily as the coalescence layer 16 is described in application US'864 cited above.
    [0046] Drop retention layer 18 is a fibrous non-woven material that has a high BET surface area, which is a BET surface area, which is at least 80% of 90 m2 / g or greater, more preferably, an area BET surface area of 95 m2 / g or greater, and more preferably, a BET surface area of 100 m2 / g or greater. The main function of the droplet retention layer is to prevent the re-emulsification of the coalesced water droplets obtained by the upstream coalescence layer 16, especially for hydrocarbons (0.025N / m). Thus, after passing through the drop retention layer 18, the coalesced water droplets will retain their coalesced size of at least 1 mm or greater. In other words, the droplet retention layer 18 will prevent the size degradation of the coalesced water droplets achieved by the coalescence layer 16.
    [0047] In this regard, the droplet retention layer can be formed from virtually any fiber it has or can be modified to have a high BET surface area. In particular, natural fibers are preferred for use as fibers to form the droplet retention layers, such as cellulose or cellulose-based fibers (eg, wood or vegetable fibers), cotton fibers, wool fibers, silk fibers, ray fibers and the like. Synthetic fibers formed from polymeric fiber forming materials can also be used, such as fibers formed from polyesters, polyamides (for example, nylon 6, nylon 6.6, nylon 6.12 and the like), polyolefins, polytetrafluoroethylene, and alcohol polyvinyl.
    [0048] In certain embodiments, the drop retention layer 18 can be a mixture of fibers having a high BET surface area and fibers having a low BET surface area. In such embodiments, it is preferable that the fibers of high surface area BET are present in an amount of at least about 59% by weight, more preferably, at least about 65% by weight of fibers of high surface area BET, the fiber balance of low BET surface area. Thus, the droplet retaining layer 18 will comprise between about 59% by weight to 100% by weight, preferably between about 65% by weight to 100% by weight of BET high surface area fibers. However, it will be understood that these bands are presently preferred embodiments of the invention, since virtually any blend of high and low surface area BET fibers can be used satisfactorily, as long as the overall non-woven medium exhibits high surface area properties. BET.
    [0049] The droplet retention layer 18 can optionally be provided with a binder resin, in order to provide increased mechanical resistance as long as the resin does not adversely affect the BET surface area of the nonwoven droplet retention layer 18. If used, it is preferable that the binder resin is one that has a polar chemical group, in order to facilitate the adsorption of water and, therefore, the separation of water from the emulsion. Suitable resin binders that can be satisfactorily employed in the droplet retention layer include, but are not limited to, phenolformaldehyde resins, polycarbonate resins, poly (acrylic acid) resins, poly (methacrylic acid) resins, polyoxide resins , polysulfide resins, polysulfone resins, polyamide resins, polyester resins, polyurethane resins, polyimide resins, poly (vinyl acetate) resins, poly (vinyl alcohol) resins, poly (vinyl chloride resins) vinyl), poly (vinylpyridine) resins, poly (vinylpyrrolidone) resins, as well as copolymers and combinations or mixtures thereof.
    [0050] The drop retention layer can be perforated or shaped (in relief), using techniques well known to people skilled in the art. Alternatively or in addition, the droplet retention layer can be treated by other suitable techniques to achieve a shape suitable for its intended end-use application. As an example, the droplet retention layer can be corrugated, curly, calendered, printed, micrexed (micrexed) and the like.
    [0051] The base weights of the coalescence layer 16 and the drop retention layers are not critical. Thus, the coalescence layer 16 and / or the droplet retention layer 18 can have a basis weight of at least about 15 grams per square meter (gsm), more preferably, at least about 35 gsm to about 300 gsm . Some embodiments of the coalescence layer 16 may have a basis weight of between about 35 to about 110 gsm.
    [0052] The optional intermediate layer (s) 20 and the confronting layers 22, 24 can be any sheet-like material that is chosen for a desired function. For example, layers 20, 22 and / or 24 can be selected to provide particle filtration (for example, to trap loose fibers and other particulate contaminants present in the liquid emulsion), in addition or alternatively to provide structural and / or protective support of coalescence layer 16 and / or drop retention layer 18. Layers 20, 22 and / or 24, therefore, do not need to be formed from a fibrous material, but could be sheets polymeric or metallic or meshes that fulfill the desired function. Suffice it to say that a person skilled in the art can envisage several multilayer structures that have the desired functional attributes for a given end-use application, as long as the water is capable of being separated from a combustible emulsion in water.
    [0053] The present invention will be further illustrated by the following non-limiting examples thereof. EXAMPLES Test methods
    [0054] Adsorption isotherms used for the application of the BET method were determined by measuring the gravimetric water absorption by each layer downstream using the following procedure.
    [0055] 1. The interior of an inert atmosphere chamber has been equilibrated to constant relative humidity through exposure to a saturated saline solution of known relative vapor pressure at a constant temperature of 21 ° C. A sensitive milligram balance was maintained inside the chamber.
    [0056] 2. Samples of downstream layers were introduced into the chamber and weighed daily until no change in weight was observed. This usually took 1-2 weeks. Final sample weights were recorded.
    [0057] 3. The saturated saline solution was replaced with a new known solution of different relative humidity and the balance / weighing process repeated.
    [0058] 4. A total of five saturated saline solutions have been used and are shown with the relative humidity in the corresponding chamber in the table below.


    [0059] 5. Upon completion of measurements for the fifth salt, samples from the downstream layer were removed from the chamber and dried in an oven at 175 ° C for five minutes and weighed.
    [0060] 6. The weight of water adsorbed on each sample at each relative humidity was calculated from the difference of the sample weight inside the chamber at each relative humidity and the weight of the sample dried in the oven.
    [0061] 7. Steps 1-6 were completed in triplicate for each layer sample downstream.
    [0062] 8. In all cases, the data obtained with potassium chloride produced a non-linear BET trace, and was excluded from use in surface area calculations. Separation medium test
    [0063] Trilayer composites were tested as separation media to separate water from a liquid emulsion of water and hydrocarbon fuel and comprised of an upstream layer (UL), a coalescence layer (CL) and an outer layer downstream (DL), in this order in relation to the flow direction of the emulsion. The media employed as the upstream layer (UL), the coalescence layer (CL) and the downstream layer (DL) in the Examples are identified by the codes in Tables 1, 2 and 3, respectively, below. Table 1 - Upstream Layer Codes




    Notes: PP = polypropylene PE = polyester PF - phenolformaldehyde PVA = polyvinyl acetate The layers used in the tri-layer composites tested were also selected for one or more functional attributes that are identified by the function codes in Table 4 below:

    [0064] The samples were tested in bench test equipment with water separator and flat sheet fuel that shape the tests of the Society of Automotive Engineers (SAE) J1488. The test equipment consisted of an emulsification circuit and a test circuit. 0.25% (2500 ppm) of distilled deionized water was emulsified at 26 - 30 ° Celsius in fuel using 1MC1E4CO a 0.75 kw mechanically coupled centrifugal pump from Gould (3.18 (i) x 2.54 (o) x 13.18 (Imp.) Cm) accelerated to a flow rate of 7.6 LPM. The resulting fuel-water emulsion flowed through the emulsification circuit which passed the emulsion through a heat exchanger and a cleaning filter bank before returning dry fuel back to the reservoir. In tests performed on B40 (40% biodiesel / 60% ULSD), the fuel was dried at 500-1500 ppm of water using a bank of four conventional separator filters run in series.
    [0065] The emulsion slip current flowed from the emulsification circuit to the test circuit. In the test circuit, emulsion was passed through the flat sheet sample holder at a nominal speed of 1.22 cm / min. The outlet from the sample holder was returned to the emulsification circuit upstream of the heat exchanger. All transfer lines upstream of the emulsion were small enough in diameter to exceed SAE J1488 speed targets. The test was performed for 90 or 150 minutes with upstream / downstream and projected reservoir samples at alternate 10 minute intervals.
    [0066] The emulsion used in the test of the examples was Ultra Low Sulfur Diesel (Diesel with ultra low sulfur content) (ULSD) Type 2D from BP Products, NA, Naperville, IL. Biodiesel was methyl soils obtained from Renewable Energy Group, Ralston, IA. The mixture used was 40 weight percent biodiesel in ULSD. According to the industry nomenclature, the resulting mixture is identified as B40. Distilled water, 3.4 umho / cm, was bottled, sodium-free, Great Value distilled water commercially available from Wal-Mart in the USA.
    [0067] The emulsion samples were homogenized for at least one minute in a Cole Parmer Ultrasonic Bath model # 08895-04. The water content was measured using a Mettler Toledo titrator model D39 Karl Fischer, and recorded in parts per million (ppm). A metric ruler inside the downstream test chamber was used to measure the size of the drops of water coming out of the medium.
    [0068] Two performance metrics were used to assess the ability to separate water from a coalescing medium, the concentration of water downstream and the size of a drop of coalescent water. Downstream water concentration is determined from Karl Fischer titration of fuel samples collected in the flow samples from the side downstream of the multilayer media. This measures the amount of water downstream of fuel from the coalescence layer in parts per million (ppm), based on mass. Clearly, the lower levels of titrated water correspond to a better performance for water withdrawal. In the case of downstream layer performance, however, the concentration of water downstream was a less important performance metric. This is the case, as the work of the downstream layer was conducted in B40 using an extremely efficient coalescence layer. Water concentrations of 400 - 600 ppm are typical for B40 mixtures with this coalescence layer. The non-woven layer downstream will not dramatically increase the expected water concentration for this coalescence layer. In addition, Karl Fischer's titrations in biodiesel mixtures have significant variation. Typically, a downstream layer was considered to have a negative impact on the water concentration downstream, when the titrated concentration rose above 800 ppm. Downstream water concentrations were measured in 10 minutes and 90 minutes from the 90 tests reported here.
    [0069] The success of any coalescence layer is dependent on the drops of coalesced water gravimetrically when it falls into a fuel counter-current on the side downstream of the medium. Many coalescence filter elements create a high-speed fuel flow on the side downstream of the coalescence element. Coalesced water droplets must be large enough to establish the high-speed flow, otherwise they will be taken for sampling, and re-fed to the fuel. This re-entry constitutes the failure of the media to coalesce water, since water is found in Karl Fischer titrations of downstream fuel samples. As such, media with a 1.0 mm drop yield are better coalescent media than those that produce 0.1 mm drops. In addition, media that create 3.0 mm drops are better than those that create 1.0 mm drops. Finally, media that do not create any drops, but produce a flow of water that flows down the face of the media or down the center of the media, are considered the best, since there are no drops available to be dragged into the flow of media. high speed fuel. Drops that are less than 1.0 mm in diameter are called "angels" in jet fuel applications. The presence of such angels on the "dry side" of a coalescing element in jet fuel is a sign of element failure.
    [0070] Coalescence media have also traditionally been found to produce foam on the downstream side. Foam production is detrimental to water separation. The foam consists of fuel-enriched water, and is less dense and more bulky than water. As a result, it resists the compaction and settling required for successful water removal. Foam fills the spaces downstream and, eventually, is easily carried by fuel sampling, re-entry of water into the fuel.
    [0071] A drop size target of 1.0 mm and larger was adjusted for the laminated trilayer media tested according to the examples. This limit was based on 1.0 - 1.7 mm coalesced water droplet sizes routinely generated by the coalescence layers used in the examples, in the absence of a downstream layer. Persistent droplet appearance <1.0 mm and foam production were considered to be failure characteristics. Absence of droplets and the creation of a stream of water below the middle face were considered a passing characteristic as if no drops were available to load in the samples. Water drop size was measured using visual inspection at 10 minutes and 90 minutes from the 90 tests used in the examples.
    [0072] The test results are shown in Table 5 below.





    2 Layer Function Codes defined in Table 4 3 Coalescent Layer Codes defined in Table 2 4 Lamination Methods: 1 = Layers pressed together with sewing adhesive at 205 ° C hot plate; 5 = layers and sewing adhesive tensioned under a curved surface with 5.0 kg by weight in 205 ° C oven 5 Layer medium codes defined in Table 3 7 Drop size was measured in 60 minutes, no data available for 90 minutes 8 Tests performed on 20% biodiesel (B20), a less severe mixture of fuel when compared to B40 9 Titration performed in 30 minutes, no data available for 10 minutes Petition 870190137336, of 12/20/2019, p. 45/58 41/41
    [0073] As the data in Table 5 show, the media in the downstream layer (DL) having a high BET surface area exhibited performance characteristics of the drop retention layer. Specifically, DL media having a BET surface area of at least 90 m2 / g or greater was sufficient to retain 1 mm or larger size of the water droplets coalesced by the coalescence layer (CL).
    [0074] Although the invention has been described in connection with what is presently considered to be the most practical and preferred modality, it is to be understood that the invention is not to be limited to the disclosed modality, but, on the contrary, it is intended to cover various modifications and equivalent arrangements included within its scope and scope.
    权利要求:
    Claims (18)
    [0001]
    1. Separation medium (14) for separating water from a water and hydrocarbon emulsion comprising surfactants, the medium comprising: a layer of fibrous non-woven coalescence (16) to receive the water and hydrocarbon emulsion and coalescing the water present in this as a discontinuous phase to obtain the coalesced water droplets having a size of 1 mm or larger; and a fibrous non-woven drop retention layer (18) downstream of the coalescence layer; characterized by said retention layer having a high BET surface area of 90 m2 / g or greater, sufficient to maintain the size of the coalesced water droplets to allow their separation from the hydrocarbon.
    [0002]
    Separation medium (14) according to claim 1, characterized by the drop retention layer (18) having a high BET surface area of 95 m2 / g or greater.
    [0003]
    Separation medium (14) according to claim 1, characterized by the drop retention layer (18) having a high BET surface area of 100 m2 / g or greater.
    [0004]
    Separation medium (14) according to claim 1, characterized by the drop retention layer (18) comprising a mixture of fibers having a high BET surface area and fibers having a low BET surface area.
    [0005]
    Separation medium (14) according to claim 1, characterized by the drop retention layer (18) comprising a resin binder.
    [0006]
    Separation medium (14) according to claim 1, characterized by the resin binder including a polar chemical group.
    [0007]
    Separation medium (14) according to claim 1, characterized in that it additionally comprises at least one additional layer (20) adjacent to one of the coalescence and drop retention layers (16, 18).
    [0008]
    Separation medium (14) according to claim 7, characterized in that at least one additional layer (20) is positioned between the coalescence and drop retention layers (16, 18).
    [0009]
    Separation means (14) according to claim 7, characterized in that the at least one additional layer (20) is positioned upstream of the coalescence layer (16).
    [0010]
    Separation medium (14) according to claim 7, characterized in that at least one additional layer (20) is positioned downstream of the drop retention layer (18).
    [0011]
    11. Separation module (10) to separate water from a water and hydrocarbon emulsion, characterized by comprising a housing (12) having an inlet (12-1) for the emulsion and respective outlets (12-2, 12-3) for dehydrated water and hydrocarbons, and a separation medium (14), as defined in claim 1, inside the housing (12).
    [0012]
    12. Method for separating water from a water and hydrocarbon emulsion in a separation medium (14), as defined in claim 1, characterized by comprising: (a) passing an emulsion of water and hydrocarbons through a coalescence layer non-woven fibrous (16) so as to coalesce the water present in it as a discontinuous phase to obtain the coalesced water droplets having a size of 1 mm or larger; (b) passing the hydrocarbon and coalesced water droplets through a droplet retention layer (18) downstream having an elevated BET surface area of 90 m2 / g or greater, sufficient to maintain the size of the coalesced water droplets; and (c) separating the coalesced water droplets from the hydrocarbon.
    [0013]
    Method according to claim 12, characterized by the hydrocarbon having an interfacial tension (y) of less than 0.025 N / m (25 dyne / cm).
    [0014]
    Method according to claim 13, characterized in that the hydrocarbon is a liquid fuel comprising a surfactant.
    [0015]
    Method according to claim 14, characterized in that the liquid fuel is a fuel comprising biodiesel.
    [0016]
    16. Method according to claim 12, characterized by step (a) being performed so that 90% or more, by weight, of the water in the emulsion is coalesced into drops of water having a droplet size of 1 mm or larger.
    [0017]
    17. Method according to claim 16, characterized by step (b) being carried out so that the coalesced water droplets maintain a droplet size of 1 mm or greater.
    [0018]
    18. Method according to claim 12, characterized by step (c) being carried out by allowing the drops of water to separate from the hydrocarbon by a difference in density between them.
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    法律状态:
    2018-04-10| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2018-08-21| B25A| Requested transfer of rights approved|Owner name: AHLSTROM-MUNKSJOE OYJ (FI) |
    2020-09-01| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-12-15| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 10 (DEZ) ANOS CONTADOS A PARTIR DE 15/12/2020, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US12/576,839|2009-10-09|
    US12/576,839|US20110084028A1|2009-10-09|2009-10-09|Separation media and methods especially useful for separating water-hydrocarbon emulsions having low interfacial tensions|
    PCT/FI2010/050777|WO2011042605A1|2009-10-09|2010-10-07|Separation media and methods especially useful for separating water-hydrocarbon emulsions having low interfacial tensions|
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